[go: up one dir, main page]

WO2019109731A1 - 复合储热材料自动化制备装置 - Google Patents

复合储热材料自动化制备装置 Download PDF

Info

Publication number
WO2019109731A1
WO2019109731A1 PCT/CN2018/110358 CN2018110358W WO2019109731A1 WO 2019109731 A1 WO2019109731 A1 WO 2019109731A1 CN 2018110358 W CN2018110358 W CN 2018110358W WO 2019109731 A1 WO2019109731 A1 WO 2019109731A1
Authority
WO
WIPO (PCT)
Prior art keywords
outlet
packaging
inlet
mixing
assembly
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/CN2018/110358
Other languages
English (en)
French (fr)
Inventor
曾智勇
徐慧芬
程勇
陈祖新
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Qinghai Enesoon New Materials Science & Technology Co Ltd
Original Assignee
Qinghai Enesoon New Materials Science & Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Qinghai Enesoon New Materials Science & Technology Co Ltd filed Critical Qinghai Enesoon New Materials Science & Technology Co Ltd
Publication of WO2019109731A1 publication Critical patent/WO2019109731A1/zh
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/60—Mixing solids with solids
    • B01F23/69—Mixing systems, i.e. flow charts or diagrams; Arrangements, e.g. comprising controlling means
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/23—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by the orientation or disposition of the rotor axis
    • B01F27/232—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by the orientation or disposition of the rotor axis with two or more rotation axes
    • B01F27/2321—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by the orientation or disposition of the rotor axis with two or more rotation axes having different inclinations, e.g. non parallel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/92—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with helices or screws
    • B01F27/922—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with helices or screws with two or more helices, e.g. with intermeshing helices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/95—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with stirrers having planetary motion, i.e. rotating about their own axis and about a sun axis
    • B01F27/953—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with stirrers having planetary motion, i.e. rotating about their own axis and about a sun axis using only helical stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B01F33/83—Mixing plants specially adapted for mixing in combination with disintegrating operations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B01F33/836—Mixing plants; Combinations of mixers combining mixing with other treatments
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/20—Measuring; Control or regulation
    • B01F35/22—Control or regulation
    • B01F35/2201—Control or regulation characterised by the type of control technique used
    • B01F35/2209—Controlling the mixing process as a whole, i.e. involving a complete monitoring and controlling of the mixing process during the whole mixing cycle
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80—Forming a predetermined ratio of the substances to be mixed
    • B01F35/88—Forming a predetermined ratio of the substances to be mixed by feeding the materials batchwise

Definitions

  • the present disclosure relates to the field of composite heat storage material preparation technology, for example, to a composite heat storage material automatic preparation device.
  • Thermal storage technology can be used to solve the contradiction between thermal energy supply and demand mismatch. It is an important technology to improve energy efficiency and protect the environment. It is widely used in the fields of solar energy utilization, “shift peak filling” of electricity, waste heat and waste heat recovery. Application prospects.
  • the composite heat storage material is a stable eutectic formed by compounding two or more inorganic salts in a certain proportion.
  • the compound compared with the raw materials alone, changes the melting point, boiling point and physical properties of the eutectic compound, improving the material properties of the original material.
  • the final composite heat storage material product entering the photothermal power station mechanism is not a monomer of a certain raw material, but a mixed eutectic salt formed by combining two or a plurality of other monomer raw materials according to a certain ratio. If you choose to purchase the monomer, in order to control the performance of the product into the organization, you first need to strictly control the quality of the raw materials, and the compounding process requires professional personnel to operate. Once the composite heat storage material product has problems in the operation process, it is difficult to compensate and define the material supplier.
  • the method for compounding the composite heat storage material is generally performed manually, and is mixed according to the proportion of each raw material in the composite heat storage material to be mixed, and the stirring device used is a conventional stirring device.
  • the various parts of the composite heat storage material production process are carried out separately and carried by hand. There is no special composite heat storage material production line in the related technology.
  • the present disclosure provides an automatic preparation device for a composite heat storage material, which can realize continuous and automatic operation of the whole process of compound heat storage material compounding.
  • An automatic preparation device for composite heat storage materials comprising:
  • the negative pressure conveying and batching mechanism comprising a plurality of branches and a first pipeline
  • the mixing mechanism includes a second conduit;
  • the inlet of the packaging mechanism is in communication with the outlet of the mixing mechanism through the second conduit, the packaging mechanism being configured to dispense the finished product;
  • An electric control mechanism is respectively connected to the negative pressure conveying and batching mechanism, the packaging mechanism and the mixing mechanism, and the electric control mechanism controls the ingredients of the negative pressure conveying and batching mechanism according to the input raw material ratio, and controls the The automatic operation of the negative pressure conveying and batching mechanism, the mixing mechanism, the packaging mechanism and the electronic control mechanism.
  • FIG. 1 is a schematic view of an apparatus for automatically preparing a composite heat storage material according to an embodiment
  • FIG. 2 is a schematic view of a compounding mechanism of a composite heat storage material automatic preparation device according to an embodiment
  • FIG. 3 is a schematic diagram of a mixing mechanism of a composite heat storage material automatic preparation device according to an embodiment
  • FIG. 4 is a schematic view of a packaging mechanism of a composite heat storage material automatic preparation device according to an embodiment
  • FIG. 5 is a schematic diagram of a granulation mechanism of a composite heat storage material automatic preparation device according to an embodiment
  • FIG. 6 is a schematic diagram of the connection of an electronic control mechanism of the composite heat storage material automatic preparation device according to an embodiment.
  • 11-unloading assembly 12-breaking assembly; 13-first pipeline; 131-first branch; 132-second branch; 133-third branch;
  • 3-packaging mechanism 31-finished silo; 32-packaging assembly; 321-first packaging production line; 322-second packaging production line; 33-screw conveyor;
  • the embodiment provides an automatic preparation device for a composite heat storage material, which comprises a negative pressure conveying and batching mechanism 1 , a mixing mechanism 2 , a packaging mechanism 3 and an electronic control mechanism 10 .
  • the negative pressure conveying and dosing mechanism 1 comprises a plurality of branches arranged to convey a plurality of raw materials to the mixing mechanism 2 according to the ratio; the inlet of the mixing mechanism 2 passes through the first line 13 and the negative pressure conveying the dosing mechanism 1
  • the outlet of the packaging mechanism 3 is connected to the outlet of the mixing mechanism 2 through the second conduit 23, and the packaging mechanism 3 is arranged to dispense the finished product; as shown in FIG.
  • the packaging mechanism 3 is connected to the mixing mechanism 2, and the electronic control mechanism 10 is arranged to control the dosing of the negative pressure conveying dosing mechanism 1 according to the input material ratio and to control the automatic operation of the above mechanism.
  • the negative pressure conveying and dosing mechanism 1 includes a discharge assembly 11 and a crushing assembly 12 which are arranged to discharge the raw materials in the tons of bags.
  • the unloading assembly 11 includes a ton bag unloading hopper and a buffer hopper. The raw materials in the ton bag are discharged to the buffer hopper through the ton bag unloading hopper.
  • the unloading assembly 11 is further A tapping mechanism is provided, and the tapping mechanism is set to tap the bag to make the raw material easy to fall.
  • a manual flapper valve is disposed below the buffer bucket, and the inlet of the crushing assembly 12 is connected to the outlet of the discharge assembly 11 and is connected or closed by a manual flapper valve.
  • the crushing unit 12 is provided with a hobbing type crusher, and the hobbing type crusher is arranged to crush the raw materials falling in the buffer bucket to make the raw material particles uniform.
  • the outlet of the crushing assembly 12 is connected to the inlet of the first conduit 13.
  • the negative pressure conveying and dosing mechanism 1 has a plurality of branches to separately feed a plurality of raw materials.
  • the first pipe 13 includes a first branch 131, a second branch 132, and a third branch 133, and each branch is respectively connected with a discharge assembly 11 and a crushing assembly 12, each branch A raw material is delivered.
  • the mixing mechanism 2 is composed of a plurality of mixing components, and a plurality of mixing components work together to improve mixing efficiency.
  • the mixing mechanism 2 is provided with three mixing components (three mixing components including a first mixing component, a second mixing component, and a third mixing component), each mixing component including a mixing bin 21 and a cone
  • the mixer 22 the inlet of the mixing silo 21 is connected to the outlet of the first pipeline 13, and the first branch 131, the second branch 132 and the third branch 133 are both connected to the mixing silo 21, and the three branches are transported.
  • the three raw materials are trapped in the mixing bin 21 through a trap installed above the mixing bin 21; the inlet of the cone blender 22 is connected to the outlet of the mixing bin 21, and the raw material trapped in the mixing bin 21 enters
  • the cone mixer 22 is mixed.
  • the cone mixer 22 is provided with two spiral cantilevers. The cantilever rotates around its own helical axis and rotates around the central axis of the conical container to sufficiently mix a variety of materials.
  • the outlet of the cone mixer 22 is connected to the inlet of the second line 23, and the finished product after the mixing is conveyed to the packaging mechanism 3 through the second line 23.
  • the process of conveying the plurality of raw materials to the mixing bin 21 by the negative pressure conveying and batching mechanism 1 is as follows:
  • each of the mixing silos 21 sequentially draws the raw materials from the three branches of the first conduit 13 in accordance with the ratio of the three raw materials.
  • the first branch 131 conveys all of the first material into the mixing bin 21 of the first mixing assembly; then, the first branch 131 delivers the first material into the mixing bin 21 of the second mixing assembly.
  • the second branch 132 conveys the second raw material into the mixing bin 21 of the first mixing assembly; the third branch 133 transports the raw material as above.
  • Each branch conveys the material of the branch in sequence to three mixing bins 21, each of which sequentially draws the raw materials of the three branches. In this way, the three mixing components separately mix the raw materials, effectively improving the mixing efficiency.
  • the mixing mechanism 2 conveys the finished finished product to the packaging mechanism 3 through the second conduit 23, which includes the finished silo 31 and the package assembly 32, and the outlet and package assembly 32 of the finished silo 31.
  • the connection, package assembly 32 is configured to quantitatively package the finished product.
  • the first packaging production line 321 and the second packaging production line 322 are disposed in the packaging assembly 32.
  • the size of the first packaging production line 321 is larger than the size of the second packaging production line 322, and the first packaging production line 321 is set.
  • a second package line 322 is provided to produce a composite heat storage material in a small package.
  • the first package production line 321 and the second package production line 322 are respectively connected to the outlet of the finished silo 31.
  • the finished product from the outlet of the finished silo 31 needs to be separately delivered to the inlet of the first packaging line 321 and the inlet of the second packaging line 322, so that the packaging mechanism 3 also sets a spiral between the finished silo 31 and the package assembly 32.
  • the conveyor 33, the auger 33 is arranged to transport the finished product to both ends of the auger 33.
  • the middle of the auger 33 is connected to the outlet of the finished silo 31, the first end of the auger 33 is a first outlet, the second end of the auger 33 is a second outlet, and the first outlet and the first packaging line 321 Connected, the second outlet is connected to the second package line 322.
  • the composite heat storage material automatic preparation device may further comprise The granulation mechanism 4, as shown in Fig. 5, the granulation mechanism 4 includes a first suction hopper 41, a granulation unit 42, and a pellet silo 43.
  • the inlet of the first suction hopper 41 is connected to the outlet of the finished silo 31, the first suction hopper 41 is arranged to suck the powder; the inlet of the granulation assembly 42 is connected to the outlet of the first suction hopper 41, and the granulation assembly 42 is arranged
  • a vacuum feeder 44 is disposed between the granulation unit 42 and the first suction hopper 41, and the vacuum feeder 44 sucks the powder in the first suction hopper 41 into the granulation unit 42.
  • the granulation unit 42 is located below the vacuum feeder 44, and the granulation unit 42 is arranged to granulate the powder falling in the vacuum feeder 44; after the granulation is completed, the granules having a diameter within a predetermined range belong to Qualified pellets, qualified pellets enter the second suction hopper 45 and are then drawn into the pellet silo 43 where the outlet of the pellet silo 43 is coupled to the inlet of the package assembly 32 to deliver the pellets to the package assembly 32. Packing.
  • the granulation assembly 42 includes a roll press 421, a granulator 422, and a linear screen 423.
  • the inlet of the roll presser 421 is connected to the outlet of the vacuum feeder 44;
  • the inlet of the granulator 422 is connected to the outlet of the roll presser 421;
  • the linear screen 423 is located below the exit of the granulator 422, the linear screen 423 Set to sieving pellets and powder.
  • the linear screen 423 includes a first screen and a second screen which are arranged in a stack, the mesh of the first screen is larger than the mesh of the second screen, and the mesh of the first screen can allow powder and qualified particles. Through the passage, the mesh of the second screen can allow the powder to pass, the diameter of the qualified pellets is smaller than the mesh of the first screen and larger than the mesh of the second screen, and the qualified pellets sieved by the linear sieve 423 are granulated.
  • the first outlet of the assembly 42 flows out and enters the pellet silo 43; the sieved powder flows out through the second outlet of the pelletizing assembly 42 and returns to the first suction hopper 41, again performing the granulation process; The pellets cannot pass through the first screen and are directly carried away by the linear screen 423.
  • a dust removing mechanism is provided, and the dust removing mechanism and the negative pressure conveying are respectively performed.
  • the dosing mechanism 1, the mixing mechanism 2, the packaging mechanism 3 and the plurality of bins of the granulating mechanism 4 are connected, and the dust removing mechanism is arranged to remove dust inside the device before the operation of the above mechanism, thereby avoiding factors affecting the purity of the finished product.
  • the automatic heat storage material automatic preparation device provided by the embodiment provides the automatic and continuous compounding of the composite heat storage material by providing the negative pressure conveying and batching mechanism 1, the mixing mechanism 2, the packaging mechanism 3 and the electronic control mechanism 10.
  • the electronic control mechanism 10 controls the batching of the negative pressure conveying and batching mechanism 1 according to the input raw material ratio, the batching process is convenient, the amount of each raw material is accurate, and the ratio is accurate; the negative pressure conveying and batching mechanism 1 is set to be more
  • the raw materials are conveyed to the mixing mechanism 2 according to the ratio; the mixing mechanism 2 mixes the plurality of raw materials; the packaging mechanism 3 is set as the finished product; and the electronic control mechanism 10 is arranged to control the automatic operation of the plurality of mechanisms.
  • Each process of the composite heat storage material automatic preparation device is continuously and automatically operated, and has high production efficiency and low labor consumption.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

一种复合储热材料自动化制备装置，负压输送配料机构，所述负压输送配料机构包括多个支路；混合机构，所述混合机构包括第一管路，所述混合机构的入口通过所述第一管路与所述负压输送配料机构的出口连接，所述负压输送配料机构设置为将多种原料根据配比输送至所述混合机构；包装机构，所述包装机构包括第二管路，所述包装机构的入口通过所述第二管路与所述混合机构的出口连通，所述包装机构设置为分装成品；及电控机构，分别与所述负压输送配料机构、所述包装机构和所述混合机构连接，所述电控机构根据输入的原料配比控制所述负压输送配料机构的配料，并控制所述负压输送配料机构、所述混合机构、所述包装机构及所述电控机构的自动化运行。

Description

复合储热材料自动化制备装置
本申请要求申请日为2017年12月07日、申请号为201711284771.8、名称为“一种复合储热材料自动化制备装置”的中国专利申请的优先权，该申请的全部内容通过引用结合在本申请中。
技术领域
本公开涉及复合储热材料制备技术领域，例如涉及一种复合储热材料自动化制备装置。
背景技术
储热技术可用于解决热能供给和需求失配的矛盾，是提高能源利用效率和保护环境的重要技术，在太阳能利用、电力的“移峰填谷”、废热和余热的回收利用等领域具有广泛的应用前景。
在中国光热发电的迅猛发展阶段，需要大量的复合储热材料作为储热及传热介质，复合储热材料是通过两种或两种以上无机盐按一定比例复配后形成的稳定共晶化合物，与单独的原材料相比，共晶化合物的交熔点、沸点及物理特性发生变化，改进了原有材料的物质特性。
进入光热电站机构的最终复合储热材料产品不是某一种原料的单体，而是二者或者其他多种单体原料按照一定比例复配后形成的混合共晶盐。如果选择采购单体，那么为了把控产品进入机构后的性能，首先需要严格控制原材料的品质，同时复配过程需要专业的人员操作。一旦复合储热材料产品在运行过程中出现了问题，则很难对材料供应商进行责任的赔偿及界定。相关技术中，进行复合储热材料复配的方法一般采用人工操作，按照所需复配的复合储热材料中各原料的比例量取后进行混合，而且，使用的搅拌装置均为常规搅拌装置，搅拌时间短则会造成搅拌不充分，不能保证产品的质量(纯度和均匀度)；时间长则不能提高效率，不能保证产品的产量，而且费时费力，成本高。此外，复合储热材料生产的各部分过程均分开进行，并由人工进行搬运，相关技术中还没有专门的复合储热材料生产线。
发明内容
本公开提供了一种复合储热材料自动化制备装置，可以实现复合储热材料 复配的整个过程连续化、自动化运行。
一种复合储热材料自动化制备装置，包括：
负压输送配料机构，所述负压输送配料机构包括多个支路及第一管路；
混合机构，所述混合机构的入口通过所述第一管路与所述负压输送配料机构的出口连接，所述负压输送配料机构设置为将多种原料根据配比输送至所述混合机构，所述混合机构包括第二管路；
包装机构，所述包装机构的入口通过所述第二管路与所述混合机构的出口连通，所述包装机构设置为分装成品；及
电控机构，分别与所述负压输送配料机构、所述包装机构和所述混合机构连接，所述电控机构根据输入的原料配比控制所述负压输送配料机构的配料，并控制所述负压输送配料机构、所述混合机构、所述包装机构及所述电控机构的自动化运行。
附图说明
图1是一实施例提供的复合储热材料自动化制备装置的示意图；
图2是一实施例提供的复合储热材料自动化制备装置的配料机构的示意图；
图3是一实施例提供的复合储热材料自动化制备装置的混合机构的示意图；
图4是一实施例提供的复合储热材料自动化制备装置的包装机构的示意图；
图5是一实施例提供的复合储热材料自动化制备装置的造粒机构的示意图；
图6是一实施例提供的复合储热材料自动化制备装置的电控机构的连接示意图。
图中：
1-负压输送配料机构；10、电控机构；
11-卸料组件；12-破碎组件；13-第一管路；131-第一支路；132-第二支路；133-第三支路；
2-混合机构；21-混合料仓；22-锥混机；23-第二管路；
3-包装机构；31-成品料仓；32-包装组件；321-第一包装生产线；322-第二包装生产线；33-螺旋输送器；
4-造粒机构；41-第一吸料斗；42-造粒机构；421-对辊压片机；422-造粒机；423-直线筛；43-粒料料仓；44-真空上料机；45-第二吸料斗。
具体实施方式
如图1所示，本实施方式提供了一种复合储热材料自动化制备装置，该复合储热材料自动化制备装置包括负压输送配料机构1、混合机构2、包装机构3和电控机构10。负压输送配料机构1包括多个支路，多个支路设置为将多种原料根据配比输送至混合机构2；混合机构2的入口通过第一管路13与负压输送配料机构1的出口连接；包装机构3的入口通过第二管路23与混合机构2的出口连通，包装机构3设置为分装成品；如图6所示，电控机构10分别与负压输送配料机构1、包装机构3和混合机构2连接，电控机构10设置为根据输入的原料配比控制负压输送配料机构1的配料并控制上述机构的自动化运行。
如图2所示，负压输送配料机构1包括卸料组件11和破碎组件12，卸料组件11设置为对吨包内的原料卸料。卸料组件11包括吨袋卸料斗和缓存斗，吨包内的原料通过吨袋卸料斗卸料至缓存斗，为了将吨包内结块的物料震碎、方便原料下落，卸料组件11还设置有拍打机构，拍打机构设置为拍打吨包，使原料便于下落。缓存斗下方设置有手动插板阀，破碎组件12的入口连接卸料组件11的出口并通过手动插板阀连通或关闭。破碎组件12设置有滚齿式破碎机，滚齿式破碎机设置为对缓存斗中下落的原料进行破碎，使原料颗粒均匀。破碎组件12的出口连接第一管路13的入口。
由于复合储热材料的制备需要使用多种原料，负压输送配料机构1具有多个支路以分别对多种原料下料。在本实施方式中，第一管道13包括第一支路131、第二支路132和第三支路133，每条支路分别连接有一个卸料组件11和破碎组件12，每一条支路对一种原料进行输送。
如图3所示，混合机构2由多个混合组件组成，多个混合组件共同作用，可以提高混合效率。在本实施方式中，混合机构2设置了三个混合组件(三个混合组件包括第一混合组件、第二混合组件及第三混合组件)，每个混合组件包括一个混合料仓21和一个锥混机22，混合料仓21的入口与第一管路13的出口连接，第一支路131、第二支路132和第三支路133均与混合料仓21连通，将三条支路输送的三种原料通过安装于混合料仓21上方的捕集器被捕集入混合料仓21中；锥混机22的入口连接混合料仓21的出口，混合料仓21中捕集的原料进入锥混机22中混合，锥混机22内设有两条螺旋设置的悬臂，悬臂在绕自身的螺旋轴线旋转的同时，还环绕锥形容器的中心轴旋转，对多种原料充分地混合。锥混机22的出口连接第二管路23的入口，通过第二管路23将混合完成后的成品输送到包装机构3。
负压输送配料机构1将多种原料输送至混合料仓21的过程如下：
输入配方后，根据三种原料的配比，每个混合料仓21从第一管路13的三个支路按照顺序吸取原料。首先，第一支路131将第一种原料全部输送入第一混合组件的混合料仓21中；然后，第一支路131将第一种原料输送入第二混合组件的混合料仓21中，与此同时，第二支路132将第二种原料输送入第一混合组件的混合料仓21中；第三支路133对原料的输送同上。每条支路按顺序将该支路的原料输送至三个混合料仓21中，每个混合料仓21按照顺序吸取三条支路的原料。如此，三个混合组件分别对原料进行混合，有效得提高了混合效率。
如图4所示，混合机构2通过第二管路23将混合完成后的成品输送到包装机构3，包装机构3包括成品料仓31和包装组件32，成品料仓31的出口与包装组件32连接，包装组件32设置为对成品定量包装。
在包装时，针对不同的包装需要，包装组件32内设置了第一包装生产线321和第二包装生产线322，第一包装生产线321的尺寸大于第二包装生产线322的尺寸，第一包装生产线321设置为生产大包装的复合储热材料，第二包装生产线322设置为生产小包装的复合储热材料。第一包装生产线321和第二包装生产线322分别与成品料仓31的出口连接。
从成品料仓31的出口出来的成品需要分别输送到第一包装生产线321的入口和第二包装生产线322的入口，因此，包装机构3还在成品料仓31和包装组件32之间设置了螺旋输送器33，螺旋输送器33设置为将成品分散运输到该螺旋输送器33两端。螺旋输送器33的中部与成品料仓31的出口连接，螺旋输送器33的第一端为第一出口，螺旋输送器33的第二端为第二出口，第一出口与第一包装生产线321连接，第二出口与第二包装生产线322连接。
由于混合机构2混合后的成品为颗粒度较小的粉料，粉料结构形态为粉状，有时需要复合储热材料产品为粒料，因此，该复合储热材料自动化制备装置还可以包括造粒机构4，如图5所示，造粒机构4包括第一吸料斗41、造粒组件42和粒料料仓43。其中，第一吸料斗41的入口与成品料仓31的出口连接，第一吸料斗41设置为吸取粉料；造粒组件42的入口与第一吸料斗41的出口连接，造粒组件42设置为对粉料造粒，在造粒组件42与第一吸料斗41之间设置有真空上料机44，真空上料机44将第一吸料斗41中的粉料吸入该造粒组件42中，造粒组件42位于真空上料机44的下方，造粒组件42设置为对真空上料机44中下落的粉料造粒；造粒完成后，直径大小处于预设范围内的粒料属于合格的粒料，合格的粒 料进入第二吸料斗45中，然后被吸入粒料料仓43，粒料料仓43的出口与包装组件32的入口连接，将粒料输送至包装组件32后进行包装。
造粒组件42包括对辊压片机421、造粒机422和直线筛423。其中，对辊压片机421的入口连接真空上料机44的出口；造粒机422的入口连接对辊压片机421的出口；直线筛423位于造粒机422的出口下方，直线筛423设置为筛分粒料和粉料。
直线筛423包括依次叠放设置的第一筛网和第二筛网，第一筛网的网孔大于第二筛网的网孔，第一筛网的网孔能允许粉料和合格的粒料通过，第二筛网的网孔能允许粉料通过，合格的粒料的直径小于第一筛网网孔且大于第二筛网网孔，直线筛423筛分的合格粒料通过造粒组件42的第一出口流出并进入粒料料仓43；筛分的粉料通过造粒组件42的第二出口流出并重新回到第一吸料斗41中，再次进行造粒过程；过大的颗粒料则不能通过第一筛网，直接由直线筛423运走。
在整个复合储热材料自动化制备装置中，由于对成品的纯度要求较高，装置内的杂质及水分等都会对成品的质量造成影响，因此，还设置有除尘机构，除尘机构分别与负压输送配料机构1、混合机构2、包装机构3和造粒机构4的多个仓室连通，除尘机构设置为在上述机构运行前对装置内部除尘，避免影响成品纯度的因素。
本实施例提供的一种复合储热材料自动化制备装置，通过设置负压输送配料机构1、混合机构2、包装机构3和电控机构10以实现复合储热材料的自动化、连续化复配。其中，电控机构10根据输入的原料配比控制所述负压输送配料机构1的配料，配料过程方便、每种原料的取量准确，配比精准；负压输送配料机构1设置为将多种原料根据配比输送至混合机构2；混合机构2将多种原料混合；包装机构3设置为分装成品；电控机构10设置为控制多个机构的自动化运行。该复合储热材料自动化制备装置的每个过程连续、自动运行，生产效率高、人力消耗少。

Claims (10)

  1. 一种复合储热材料自动化制备装置，包括：
    负压输送配料机构(1)，所述负压输送配料机构(1)包括多个支路；
    第一管路(13)；
    混合机构(2)，所述混合机构(2)的入口通过所述第一管路(13)与所述负压输送配料机构(1)的出口连接，所述负压输送配料机构(1)设置为将多种原料根据配比输送至所述混合机构(2)；
    第二管路(23)；
    包装机构(3)，所述包装机构(3)的入口通过所述第二管路(23)与所述混合机构(2)的出口连通，所述包装机构(3)设置为分装成品；及
    电控机构(10)，分别与所述负压输送配料机构(1)、所述包装机构(3)和所述混合机构(2)连接，所述电控机构(10)设置为根据输入的原料配比控制所述负压输送配料机构(1)的配料，并控制所述负压输送配料机构(1)、所述混合机构(2)、所述包装机构(3)及所述电控机构(10)的运行。
  2. 根据权利要求1所述的复合储热材料自动化制备装置，其中，所述负压输送配料机构(1)包括：
    卸料组件(11)，所述卸料组件(11)设置为对吨包内的原料卸料；及
    破碎组件(12)，所述破碎组件(12)的入口连接所述卸料组件(11)的出口，所述破碎组件(12)的出口连接所述第一管路(13)的入口。
  3. 根据权利要求1所述的复合储热材料自动化制备装置，其中，所述混合机构(2)包括多个混合组件，所述混合组件包括：
    混合料仓(21)，所述混合料仓(21)的入口与所述第一管路(13)的出口连接；及
    锥混机(22)，所述锥混机(22)的入口连接所述混合料仓(21)的出口，所述锥混机(22)的出口连接所述第二管路(23)的入口。
  4. 根据权利要求1所述的复合储热材料自动化制备装置，其中，所述包装机构(3)包括成品料仓(31)和包装组件(32)，所述成品料仓(31)的入口连接所述第二管路(23)的出口，所述包装组件(32)设置为与所述成品料仓(31)的出口连接，并对成品定量包装。
  5. 根据权利要求4所述的复合储热材料自动化制备装置，其中，所述包装组件(32)包括第一包装生产线(321)和第二包装生产线(322)，所述第一包装生产线(321)的尺寸大于第二包装生产线的尺寸，所述第一包装生产线(321) 和所述第二包装生产线(322)均分别与所述成品料仓(31)的出口连接。
  6. 根据权利要求5所述的复合储热材料自动化制备装置，其中，所述包装机构(3)还包括设置于所述成品料仓(31)和所述包装组件(32)之间的螺旋输送器(33)，所述螺旋输送器(33)的入口与所述成品料仓(31)的出口连接，所述螺旋输送器(33)包括第一出口和第二出口，所述第一出口与所述第一包装生产线(321)连接，所述第二出口与所述第二包装生产线(322)连接。
  7. 根据权利要求6所述的复合储热材料自动化制备装置，还包括造粒机构(4)，所述造粒机构(4)包括：
    第一吸料斗(41)，所述第一吸料斗(41)的入口与所述成品料仓(31)的出口连接，所述第一吸料斗(41)设置为吸取粉料；
    造粒组件(42)，所述造粒组件(42)的入口与所述第一吸料斗(41)的出口连接，所述造粒组件(42)对粉料造粒；及
    粒料料仓(43)，所述粒料料仓(43)的入口与所述造粒组件(42)的出口连接，粒料料仓(43)设置为接收粒料，所述粒料料仓(43)的出口与所述包装组件(32)的入口连接，粒料料仓(43)还设置为将粒料输送至所述包装组件(32)进行包装。
  8. 根据权利要求7所述的复合储热材料自动化制备装置，其中，所述造粒组件(42)包括：
    对辊压片机(421)，所述对辊压片机(421)的入口连接所述第一吸料斗(41)的出口；
    造粒机(422)，所述造粒机(422)的入口连接所述对辊压片机(421)的出口；及
    直线筛(423)，所述直线筛(423)位于所述造粒机(422)的出口下方，直线筛(423)设置为筛分粒料和粉料。
  9. 根据权利要求8所述的复合储热材料自动化制备装置，其中，所述直线筛(423)包括依次叠放设置的第一筛网和第二筛网，所述第一筛网的网孔大于所述第二筛网的网孔，所述第一筛网的网孔设置为供粉料和直径大小处于预设范围内的粒料通过，所述第二筛网的网孔设置为供粉料通过，所述造粒组件(42)的第一出口与所述粒料料仓(43)的入口连接，所述造粒组件(42)设置为将所述直线筛(423)筛分的直径大小处于预设范围内的粒料输送至所述粒料料仓(43)，所述造粒组件(42)的第二出口与所述第一吸料斗(41)的入口连接， 所述造粒组件(42)还设置为将所述直线筛(423)筛分的粉料输送至所述第一吸料斗(41)。
  10. 根据权利要求7所述的复合储热材料自动化制备装置，还包括除尘机构，所述除尘机构分别与所述负压输送配料机构(1)、所述混合机构(2)、所述包装机构(3)和所述造粒机构(4)的多个仓室连通。
PCT/CN2018/110358 2017-12-07 2018-10-16 复合储热材料自动化制备装置 Ceased WO2019109731A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201711284771.8A CN107824064A (zh) 2017-12-07 2017-12-07 一种复合储热材料自动化制备装置
CN201711284771.8 2017-12-07

Publications (1)

Publication Number Publication Date
WO2019109731A1 true WO2019109731A1 (zh) 2019-06-13

Family

ID=61642015

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2018/110358 Ceased WO2019109731A1 (zh) 2017-12-07 2018-10-16 复合储热材料自动化制备装置

Country Status (2)

Country Link
CN (1) CN107824064A (zh)
WO (1) WO2019109731A1 (zh)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111037775A (zh) * 2019-12-30 2020-04-21 广东国珑新材料科技有限公司 一种阻燃材料全自动生产线
CN111545103A (zh) * 2020-05-13 2020-08-18 郭保林 一种粉料配比混合的方法
CN113148682A (zh) * 2021-04-27 2021-07-23 哈尔滨创博智能装备有限公司 一种吨包卸料机
CN113698070A (zh) * 2021-08-09 2021-11-26 郑州旭飞光电科技有限公司 用于玻璃配合料的混合设备
CN114146618A (zh) * 2021-12-02 2022-03-08 江苏阿路美格新材料股份有限公司 一种防火芯卷生产线的自动化配料系统
CN114797648A (zh) * 2022-06-02 2022-07-29 威海泓创企业管理咨询有限公司 一种超细精粉全封闭智能准混配装置
CN115946236A (zh) * 2021-10-08 2023-04-11 江苏苏嘉集团新材料有限公司 耐火砖生产线、生产控制系统、自动配料系统
CN116870769A (zh) * 2023-08-01 2023-10-13 山东土秀才生物科技有限公司 一种肥料生产系统

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107824064A (zh) * 2017-12-07 2018-03-23 青海爱能森新材料科技有限公司 一种复合储热材料自动化制备装置
CN111728243B (zh) * 2020-06-23 2025-01-28 安徽省天可饲料有限公司 一种饲料加工设备

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102218364A (zh) * 2011-01-13 2011-10-19 抚州聚源硅业有限公司 一种高化学活性低细粉率金属硅粉的制备工艺及专用设备
CN103937464A (zh) * 2013-12-26 2014-07-23 深圳市爱能森科技有限公司 一种高温熔盐制备装置及方法
CN104999565A (zh) * 2015-08-07 2015-10-28 江苏沃尔夫机械有限公司 一种高精度的干混砂浆生产线智能化电气控制系统
US20160121286A1 (en) * 2014-11-04 2016-05-05 The Procter & Gamble Company Apparatus and process for forming particles
CN105664761A (zh) * 2016-01-07 2016-06-15 南昌理工学院 一种调味品自动化生产设备
CN205386437U (zh) * 2016-02-24 2016-07-20 秦皇岛三农现代化机械设备有限公司 对辊挤压造粒机系统
CN206688553U (zh) * 2016-12-12 2017-12-01 青海爱能森新材料科技有限公司 一种储热熔盐搅拌装置
CN107824064A (zh) * 2017-12-07 2018-03-23 青海爱能森新材料科技有限公司 一种复合储热材料自动化制备装置

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101987800B (zh) * 2010-08-09 2013-06-26 江阴市联业生物科技有限公司 Bb肥生产方法及其专用设备
CN103214295A (zh) * 2013-02-25 2013-07-24 龚水明 一种生物质锅炉灰渣有机肥生产工艺
CN207641314U (zh) * 2017-12-07 2018-07-24 青海爱能森新材料科技有限公司 一种复合储热材料自动化制备装置

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102218364A (zh) * 2011-01-13 2011-10-19 抚州聚源硅业有限公司 一种高化学活性低细粉率金属硅粉的制备工艺及专用设备
CN103937464A (zh) * 2013-12-26 2014-07-23 深圳市爱能森科技有限公司 一种高温熔盐制备装置及方法
US20160121286A1 (en) * 2014-11-04 2016-05-05 The Procter & Gamble Company Apparatus and process for forming particles
CN104999565A (zh) * 2015-08-07 2015-10-28 江苏沃尔夫机械有限公司 一种高精度的干混砂浆生产线智能化电气控制系统
CN105664761A (zh) * 2016-01-07 2016-06-15 南昌理工学院 一种调味品自动化生产设备
CN205386437U (zh) * 2016-02-24 2016-07-20 秦皇岛三农现代化机械设备有限公司 对辊挤压造粒机系统
CN206688553U (zh) * 2016-12-12 2017-12-01 青海爱能森新材料科技有限公司 一种储热熔盐搅拌装置
CN107824064A (zh) * 2017-12-07 2018-03-23 青海爱能森新材料科技有限公司 一种复合储热材料自动化制备装置

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111037775A (zh) * 2019-12-30 2020-04-21 广东国珑新材料科技有限公司 一种阻燃材料全自动生产线
CN111545103A (zh) * 2020-05-13 2020-08-18 郭保林 一种粉料配比混合的方法
CN113148682A (zh) * 2021-04-27 2021-07-23 哈尔滨创博智能装备有限公司 一种吨包卸料机
CN113698070A (zh) * 2021-08-09 2021-11-26 郑州旭飞光电科技有限公司 用于玻璃配合料的混合设备
CN115946236A (zh) * 2021-10-08 2023-04-11 江苏苏嘉集团新材料有限公司 耐火砖生产线、生产控制系统、自动配料系统
CN114146618A (zh) * 2021-12-02 2022-03-08 江苏阿路美格新材料股份有限公司 一种防火芯卷生产线的自动化配料系统
CN114797648A (zh) * 2022-06-02 2022-07-29 威海泓创企业管理咨询有限公司 一种超细精粉全封闭智能准混配装置
CN116870769A (zh) * 2023-08-01 2023-10-13 山东土秀才生物科技有限公司 一种肥料生产系统

Also Published As

Publication number Publication date
CN107824064A (zh) 2018-03-23

Similar Documents

Publication Publication Date Title
WO2019109731A1 (zh) 复合储热材料自动化制备装置
CN203851780U (zh) 一种全价饲料生产线
CN103734886A (zh) 饲料自动配料系统及其生产工艺
CN108654581B (zh) 一种吸附剂物料的连续混合、造粒与干燥装置
CN107878789A (zh) 一种螺杆挤压粉料造粒系统及造粒工艺
CN106287732A (zh) 多物态危废焚烧预处理与配伍系统及方法
CN204996407U (zh) 一种干法制粒生产装置
CN110591417A (zh) 一种废轮胎裂解炭黑的连续化进料造粒装置
CN203227462U (zh) 配料混合装置
CN105642392A (zh) 一种槽料机
CN211025984U (zh) 一种复合石墨电极配料混合装置
CN108837931B (zh) 一种中药精华素无尘密闭的粉碎系统
CN207641314U (zh) 一种复合储热材料自动化制备装置
CN213557402U (zh) 炭黑粉末造粒系统
CN206855813U (zh) 一种造粒机
CN107469691A (zh) 一种配肥设备
CN205547294U (zh) 肉牛料循环生产设备
WO2019109286A1 (zh) 复合储热材料自动化制备装置
CN107441983A (zh) 一种搅拌机构和配肥设备
CN206073081U (zh) 多物态危废焚烧预处理与配伍系统
CN217796005U (zh) 制粒装置及颗粒剂连续生产系统
CN204890651U (zh) 一种风湿骨痛片混合制粒压片设备
CN206215534U (zh) 一种筛分配料系统
CN204890609U (zh) 一种健胃消食片混合制粒压片机
CN107486077A (zh) 一种配肥设备

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 18886879

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 18886879

Country of ref document: EP

Kind code of ref document: A1